US2012258269A1PendingUtilityA1
Preparing polyester polyols
Est. expiryDec 16, 2029(~3.4 yrs left)· nominal 20-yr term from priority
C08G 18/4238C08G 63/12C08G 18/08C08G 18/7671C08K 5/524C08G 63/78Y10T428/139C08G 63/16C08G 18/664C08G 18/00C08G 18/42
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Claims
Abstract
A process for preparing a polyester polyol comprises the steps of: (a) preparing a reaction mixture comprising the following components: A: at least one carboxylic acid recovered from natural raw materials and having at least two acid groups, B: at least one polyhydric alcohol, C: at least one organic phosphite compound, D: at least one Lewis acid; (b) heating the reaction mixture to a temperature of at least 160° C. and removing the water formed in the course of the reaction; (c) heating the reaction mixture to a temperature of at least 210° C. under a pressure below 1013 mbar for a period of time in the range from 0.1 to 25 hours.
Claims
exact text as granted — not AI-modified1 . A process for preparing a polyester polyol, the process comprising of:
(a) preparing a reaction mixture comprising:
A: at least one carboxylic acid recovered from a natural raw material and having at least two acid groups, selected from the group consisting of sebacic acid, azelaic acid, dodecanedioic acid and succinic acid,
B: at least one polyhydric alcohol,
C: at least one organic phosphite compound,
D: at least one Lewis acid;
(b) heating the reaction mixture to a temperature of at least 160° C. and removing water formed during a reaction; and (c) heating the reaction mixture to a temperature of at least 210° C. at a pressure below 1013 mbar for 0.1 to 25 hours, to obtain a polyester polyol.
2 . The process of claim 1 wherein (a) comprises first mixing A, B and D, and then adding C.
3 . (canceled)
4 . The process of claim 1 , wherein A comprises sebacic acid recovered from a renewable raw material.
5 . The process of claim 1 , wherein B comprises an aliphatic C 2 to C 6 diol.
6 . The process of claim 1 , wherein B comprises 1,3-propanediol or 1,4-butanediol.
7 . The process of claim 1 , wherein C comprises at least one organic phosphite compound selected from the group consisting of bis(2,4-di-tert-butyl-6-methylphenyl)ethyl phosphite, tris(nonylphenyl)phosphite or a reaction product of phosphorus trichloride with 1,1′-biphenyl and 2,4-bis(tert-butyl)phenol.
8 . The polyester polyol obtained by the process of claim 1 .
9 . The polyester polyol of claim 8 wherein A comprises sebacic acid recovered from a renewable raw material, and B comprises a diol.
10 . A process for preparing a polyurethane by reacting the polyester polyol obtained by the process claim 1 with one or more organic diisocyanates.
11 . A thermoplastic polyurethane obtained by the process of claim 10 .
12 . (canceled)
13 . A process of manufacturing a molding, a hose, a self-supporting film/sheet, or a fiber, the process comprising the process of claim 10 .
14 . A molding, a self-supporting film/sheet, a hose or a fiber comprising the thermoplastic polyurethane of claim 11 .
15 . The process of claim 1 , wherein (c) is performed for 5 to 20 hours.
16 . The process of claim 1 , wherein B comprises 1,3-propanediol.
17 . The process of claim 1 , wherein B comprises 1,4-butanediol.
18 . The process of claim 1 , wherein D is selected from the group consisting of titanium tetrabutoxide, titanium tetraisopropoxide, tin dioctoate, dibutyltin laurate, and tin chloride.
19 . The process of claim 1 , wherein the polyester polyol obtained has a color number between 10 and 200 APHA/HAZEN.
20 . The process of claim 1 , wherein the polyester polyol obtained has an acid number less than 3 g KOH/kg.
21 . The process of claim 1 , wherein the polyester polyol obtained has an acid number less than 1 g KOH/kg.
22 . The process of claim 1 , performed without a solvent.Cited by (0)
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